Research Article. Experimental studies of an antibacterial agent on the corrosion of mild steel in 1M H 2 SO 4

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1 Available online Journal of Chemical and Pharmaceutical Research, 2015, 7(1): Research Article ISSN : CODEN(USA) : JCPRC5 Experimental studies of an antibacterial agent on the corrosion of mild steel in 1M H 2 SO 4 S. Karthikeyan*, P. A. Jeeva and K. Raja School of Mechanical and Building Sciences, VIT University, Vellore, Tamilnadu, India ABSTRACT Corrosion behavior of mild steel in 1M Sulphuric acid with an anti-bacterial agent, viz., Vancomycin as corrosion inhibitor has been studied by using mass loss, potentiodynamic polarization, electrochemical impedance spectroscopy and hydrogen permeation studies. All these techniques reveal that inhibition efficiency increases with the increase in the concentration of antibacterial agent. Polarization studies indicated that inhibitor acted as cathodic inhibitor. It was found that the adsorption of green inhibitor on the mild steel surface obeying Langmuir adsorption isotherm. Keywords: Mild Steel; Corrosion Inhibition; vancomycin; Adsorption Isotherm; Green inhibitor INTRODUCTION Mild steel is an important class of metals due to its outstanding mechanical properties. It is widely used under different conditions in chemical and allied industries in handling acidic, alkaline and salt solutions. Mild steel is used in industries as pipelines for petroleum industries, storage tanks, reaction vessel and chemical batteries [1]. Acid solutions are widely used in many industrial processes like acid cleaning, pickling and descaling due to their chemical properties [2-5]. Acids cause damage to the steel substrate, because of their corrosive nature. Several methods were used to reduce the corrosion of metals in acidic medium, but the use of inhibitors is most widely employed[ 6-10]. Organic compounds are widely used as corrosion inhibitors for mild steel in acidic media [11-16]. The rate of corrosion retards by adsorption of organic inhibitors on the mild steel surface. The inhibitors block the reactive parts by replacing water molecules and form a dense barrier layer on the metal surface. The majority of the organic inhibitors are toxic, highly expensive and non environment friendly. Research activities in recent times are booming on developing the cheap, non-toxic drugs as environment friendly corrosion inhibitors [17-21]. The aim of this study is to examine the corrosion protection efficacy of vancomycin for mild steel corrosion in 1M H 2 SO 4. We came to know no concrete report is available for the use this compound as corrosion inhibitor in 1M H 2 SO 4. From the literature the higher concentration of H 2 SO 4 acts as pickling solution for mild steel for electroplating, battery electrodes using sulfur containing organic compounds. Use of these inhibitors in 1M H 2 SO 4 will reduce the metal loss in acid medium. The antibacterial drug is of glycopeptide antibiotic used to treat infections in intestine. The inhibition efficiency of this green inhibitor was monitored using mass loss measurement, potentiodynamic polarization studies, impedance techniques, hydrogen permeation studies and diffuse reflectance methods. 906

2 EXPERIMENTAL SECTION 2.1. Materials Mild steel specimens of size 1x4 cm 2 were used for weight loss and electrochemical studies. The aggressive solution of 1M H 2 SO 4 (AR Grade) was used for all the studies. The antibiotic namely vancomycin was purchased from the medicine shop and used as such. The structures of the antibiotics are given in the figure 1. Figure 1. Structure of Vancomycin The IUPAC name of Vancomycin is (1S,2R,18R,19R,22S,25R,28R,40S)- 48- {[(2S,3R,4S,5S,6R)- 3- {[(2S,4S,5S,6S)- 4- amino- 5- hydroxy- 4,6- dimethyloxan- 2- yl]oxy}- 4,5- dihydroxy- 6- (hydroxymethyl)oxan- 2- yl]oxy}- 22- (carbamoylmethyl)- 5,15- dichloro- 2,18,32,35,37- pentahydroxy- 19- [(2R)- 4- methyl- 2- (methylamino) pentanamido]- 20,23,26,42,44- pentaoxo- 7,13- dioxa- 21,24,27,41,43- pentaazaoctacyclo[ ,6.214,17.18,12.129,33.010,25.034,39]pentaconta 3,5,8(48),9,11,14,16, 29 (45), 30, 32, 34, 36,38,46,49- pentadecaene- 40- carboxylic acid. Electrochemical experiments were cariedout using a three electrode cell assembly with mild steel samples as working electrode, 4cm 2 area of platinum as counter electrode and Hg/Hg 2 SO 4 /1M H 2 SO 4 as the reference electrode. The surfaces of corroded and corrosion inhibited mild steel specimens were examined by diffuse reflectance studies in the region nm using U-3400 spectrometer (UV-VIS-NIR Spectrometer, Hitachi, Japan) Mass loss studies The concentrations of inhibitor used for weight loss and electrochemical study were from 25x10-4 M to 75x10-4 M. Mild steel specimens of size 1x4 cm 2 were abraded with different emery papers and degreased with trichloroethylene. The cleaned samples were then washed with double distilled water and finally dried and kept in the desicator. The mass loss study was carried out at room temperature for 3 hours in 1M H 2 SO 4. The experiments were performed in triplicate. The inhibition efficiency (IE %) was determined by the following equation Inhibition Efficiency (IE %) = (W 0 W i /W 0 ) X 100 Where W 0 & W i are the mass loss values in the absence and presence of vancomycin Electrochemical studies Potentiodynamic polarization measurements were done out in a conventional three electrode cylindrical glass cell, using CH electrochemical analyzer. The solution was deaerated for 20 minute before carryout the polarization studies. The working electrode was kept at its corrosion potential for 10 min. until a steady state was achieved. The mild steel surface was exposed to various concentrations of inhibitor in 100mL of 1M H2SO4 at room temperature. The inhibition efficiency (IE %) was calculated using the equation. 907

3 Inhibition Efficiency (IE %) = (I 0 I /I 0 ) X 100 Where I 0 and I are the corrosion current density without and with the inhibitor respectively. The potentiodynamic current-potential curves were noted by changing the electrode potential automatically from - 750mV to +150mV versus the open circuit potential. The corresponding corrosion current (I corr ) was recorded. Tafel plots were built by plotting E versus log I. Corrosion Potential (E corr ), corrosion current density (I corr ) and cathodic and anodic slopes (β c and β a ) were calculated according to known procedures. Impedance measurements were performed in the frequency range from 0.1 to Hz using amplitude of 20 mv and 10 mv peak to peak with an AC signal at the open-circuit potential. The impedance diagrams were plotted in the nyquist representation. Charge transfer resistance (R ct ) and double layer capacitance (C dl ) values were acquired from nyquist plot [25, 26]. The percentage inhibition efficiency was calculated from the equation Inhibition Efficiency (IE%) = ( C dl - C dl / C dl ) x 100 Where C dl and C dl are the corrosion current of mild steel with and without inhibitor respectively Hydrogen permeation studies The hydrogen permeation study was monitored using an adaptation of modified Devanathan and Stachurski s, two compartment cell as described elsewhere [27]. Hydrogen permeation currents were noted in the absence and presence of inhibitors Diffuse reflectance spectroscopy The surfaces of corroded and corrosion inhibited mild steel specimens were scrutinized by diffuse reflectance studies in the region nm using U-3400 spectrometer [UV-VIS-NIR Spectrometer, Hitachi, Japan]. RESULTS AND DISCUSSION 3.1. Mass loss studies The values of inhibition efficiency (IE%),corrosion rate (CR) and surface coverage(θ) calculated for vancomycin in 1M H 2 SO 4 at different concentrations from the mass loss data are summarized in the table-1. It is noticeable that inhibition efficiency boosts with increase in the inhibitor concentration. In addition the rate of corrosion has reduced with increase in inhibitor concentration. Maximum inhibition efficiency is obtained at 75x10-4 M concentrations of the inhibitor. Table 1. Values of Inhibition Efficiency, Corrosion rate and Surface coverage for the corrosion of mild steel in 1M H 2SO 4 in presence of different concentrations of Vancomycin from mass loss measurements. Inhibitor Conc. (M) Inhibition Efficiency Surface Coverage [θ] Blank - - Vancomycin 25x x x Potentiodynamic polarization studies Polarization plots for mild steel in 1M H 2 SO 4 containing different concentrations of green inhibitor for two antibiotics are summarized in table -2. The values of corrosion potential (E corr ), corrosion current densities (I corr ), anodic Tafel slope (β a ),cathodic Tafel slope (β c ) surface coverage(θ) and inhibition efficiency (IE%) were calculated using polarization curves. According to the results, corrosion current (I corr ) value diminishes with increase in the concentration of the Vancomycin drug. The inhibition efficiency (IE %) and surface coverage (θ) increases with increase in inhibitor concentration for all the three antibiotics. The maximum inhibition efficiency was achieved at 75x10-4 M concentration of the inhibito. It has been observed that both βa and β c are reduced, but the values of β c are decreased to a greater extent. This indicates that the compound behaved as cathodic inhibitor. 908

4 Table 2: Electrochemical parameters and Inhibition Efficiency for corrosion of mild steel in 1M H 2SO 4 obtained by Polarization method in presence of different concentrations of vancomycin drug. Inhibitor Con. [M] E corr [mv vs SCE] I corr [µa cm -2 ] β a [mv dec -1 ] β c [mv dec -1 ] Inhibiton efficiency [%] Surface coverage [θ] Blank Vancomycin 25x x x Electrochemical impedance studies Values of charge transfer resistance (R ct ) and double layer capacitance (C dl ) derived from Nyquist plots are shown in table 3. The values of R ct are appeared to increase with increase in concentration of inhibitors in 1M H 2 SO 4. It is cleared that values of C dl are fetched down by increasing concentrations of inhibitors in the acid. This can be attributed to the dominant adsorption of the green inhibitor on the mild steel surface. Table 3: Electrochemical parameters and Inhibition efficiency for corrosion of mild steel in 1M H 2SO 4 obtained by Impedance method in presence of different concentrations of vancomycin drug. Inhibitor Con. [M] R ct [Ω cm 2 ] C dl [F cm -2 ] Inhibition efficiency [%] Surface coverage[θ] Blank Cloxacillin 25x x x Figure 2: UV Reflectance curves of mild steel in 1M H 2SO 4 solution with various Concentrations of the inhibitor UV spectral reflectance studies The reflectance plots for polished specimen, specimen dipped in 1M H 2 SO 4 and various concentrations of vancomycin are given in the figure.2. The percentage of reflectance is maximum for polished mild steel and it 909

5 progressively diminishes for the specimen dipped in 1M H 2 SO 4 solution. This observation unveils that the change in surface property is due to the corrosion of mild steel in acid. Also the reflectance percentage of steel in the presence of green inhibitor is higher than steel as immersed in blank. This endorses that the surface property of steel has not transformed further due to the formation of protective layer on the mild steel surface. The reflectance percentage declines with increase in thickness of the inhibitor film formed on metal surface. A similar finding has been made by Madhavan etal [29] Adsorption isotherm and thermodynamic parameters The inhibitive action of inhibitor in extremely belligerent media is due to its adsorption on the metal surface. The degree of surface Coverage (θ) for different concentrations of vancomycin in 1M H 2 SO 4 has been calculated from mass loss, polarization and electrochemical impedance studies. The attained data was tested graphically for fitting suitable isotherm [30-32]. Almost a straight line was obtained by plotting log (C/θ) Vs log C shown in Figure-3, which demonstrates that the adsorption of these compounds on steel surface observes Langmuir adsorption isotherm. The Langmuir isotherm for the adsorbed layers is given by the equation [33], C inh /θ =1/K ads + C inh Where K ads is the equilibrium constant of the adsorption/desorption process. Adsorption equilibrium constant [K ads ] and free energy of adsorption [ G 0 ads] were calculated using the equation 34 K ads = 1/C inh x θ/1-θ G 0 ads = RT log [55.5K ads ] Where 55.5 is the molar concentration of water in solution [35]. R is the gas constant, T is the temperature. The values of adsorption equilibrium constant [K ads ] and free energy of adsorption [ G 0 ads] are given in table-4. The negative values of [ G 0 ads] pointed out that adsorption of inhibitor is spontaneous process. It is reported that values of [ G 0 ads] is of order 20 kjmol -1 or lower indicates a physisorption, those of order of -40kJmol -1 or higher involve charge sharing or transfer from the inhibitors to the metal surface specifies a chemisorptions [36-38]. The values of free energy of adsorption [ G 0 ads] in our experiment lies in the range -28 to -32 kjmol -1, signifying that the adsorption is not a simple physisorption, but it may contain some other interactions [39]. Table 4: Gibbs free energy parameters and adsorption equilibrium constant [K] of green inhibitor at various temperatures evaluated by weight loss method. Temperature (K) Vancomycin Kads - G 0 ads (kjmol -1 ) Hydrogen permeation measurements Hydrogen permeation currents are recorded in H 2 SO 4 in the absence and presence of vancomycin drug. This study has been taken up with a plan of selecting the inhibitors with a view to their effectiveness on the lessening of hydrogen uptake 40. The values of permeation current with respect to time are given in table-5. The inhibitor brings down the permeation current to the extent of 50%. Thus a definite correlation exists between the corrosion inhibition efficiency and the extent of reduction in the permeation current of this compound. It is a known fact that lower β c value for an inhibiting compound, the smaller is the corrosion and hydrogen ingress on the metal. An increase in the β c value, leads to rise in the energy barrier for proton discharge and increase in the evolution of hydrogen. This in turn leads to higher entry of hydrogen through the steel surface Mechanism of corrosion inhibition The adsorption of vancomycin onto the mild steel surface is found to be majorly physical in nature. Physical adsorption is a process of electrostatic attraction between charged species in the solution and the metal surface. If the metal surface is positively charged, the adsorption of negatively charged species is facilitated. Positively charged species can also adsorb on the positively charged metal surface with the help of negatively charged intermediate, which adsorb first on the positively charged metal surface and allows positively charged species to adsorb on it. 910

6 Table 5: Values of permeation current for mild steel in 1M H 2SO 4 and in presence of green inhibitor with respect to change in time Permeation Current (µa) Time (min.) 1M H 2SO 4 Vancomycin Thus the adsorption of vancomycin may take place in two different ways as (i) The protonated vancomycin in acid solution may adsorb electro statically to the anion covered mild steel surface through their protonated form. (ii) The inhibitors may compete with acid anions for the sites at the water covered surface and adsorb by donating electrons to the mild steel surface [40-42]. CONCLUSION 1. The use of Vancomycin antibiotic as green corrosion inhibitor in 1M H 2 SO 4 was thoroughly studied using mass loss, potentiodynamic polarization, impedance measurements and hydrogen permeation studies. 2. The adsorption of green inhibitor on mild steel surface follows Langmuir adsorption isotherm. The adsorption of compounds on steel surface is further confirmed by diffuse reflectance spectra. REFERENCES [1] J Zhang; J Liu;W Yu;Y Yan; L You; L Liu. Corros. Sci., 2010, 52(6), [2] IB Obot; NO Obi-Egbedi; SA Umoren. Int. J. Electrochem. Sci., 2009, 4, [3] S Vishwanatham; Anil Kumar. Corros. Rev., 2005, 23, [4] NO Eddy; EE Ebenso; UJ Ibok. J. Appl. Electrochem., 2010, 40(2), [5] EE Ebenso; H Alemu; SA Umoren; IB Obot, Int. J. Electrochem. Sci., 2008, 3, [6] SK Shukla; MA Quraishi; R Prakash. Corros. Sci., 2008, 50(10), [7] MW Ranney. Inhibitors Manufacture and Technology, 1976, Noyes Data Corp: NJ. [8] AK Singh; SK Shukla; M Singh; MA Quraishi. Mater. Chem. Phys., 2011, 129, [9] SK Shukla; MA Quraishi. Mater.Chem. Phys., 2010, 120(1), [10] NO Eddy; EE Ebenso. Afri J of Pure & Appl Chem., 2008, 2(6), 1-9. [11] M Lagrenee ; B Mernari; M Bouanis; M Traisnel; F Bentiss. Corros Sci., 2002, 44(3), [12] MA Quraishi; S Khan. J Appl Electrochem., 2006, 36(5), [13] MA Quraishi; M Athar; H Ali. Br Corros J, 2002, 37(2), [14] R Hasanov; M Sadikoglu; S Bilgic. Appl. Surf. Sci., 2007, 253, [15] A Chetouani; B Hammouti; T Benhadda; M Daoudi. Appl. Surf. Sci., 2005, 249, [16] M Bouklah; B Hammouti; M Lagrenee; F Bentiss. Corros. Sci., 2006, 48(9), [17] M Abdallah. Corros Sci., 2002, 44(4), [18] M Abdallah, Corros Sci., 2004, 46, [19] MM El-Naggar. Corros Sci., 2004, 49(5), [20] R Solmaz; G Kardas; B Yazici; M Erbil, Protection of Metals, 2005, 41(6), [21] WT Sing; CL Lee; SL Yeo; SP Lim; MM Sim. Bioorg Med Chem Lett., 2001, 11, [22] O Nnabuk Eddy; E Eno Ebenso; J Udo Ibok. J Appl Electrochem., 2010, 40(2), [23] Nnabuk O. Eddy; Udo J. Ibok; Eno E. Ebenso; Ahmed El Nemr; El Sayed H. ElAshry. J Mol Model., 2009, 15(9), [24] OE Nnabuk; AA Siaka; AF Atiku; A Muhmmad. Innovations in Science and Engineering, 2011, 1, [25] F Bentiss; M Lagrenee; M Traisnel; JC Hornez. Corros Sci., 1999, 41(4), [26] H Ashassi-Sorkhabi; B Shaabani; Seifzadeh. Electrochim Acta, 2005, 50(16), [27] MAV Devanathan; Z Stachurski. Proc.Roy.Soc., 1962, 270 A,

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